CN1323755C - Method for preparing hydrogenation aromatization catalyst - Google Patents
Method for preparing hydrogenation aromatization catalyst Download PDFInfo
- Publication number
- CN1323755C CN1323755C CNB2004100605763A CN200410060576A CN1323755C CN 1323755 C CN1323755 C CN 1323755C CN B2004100605763 A CNB2004100605763 A CN B2004100605763A CN 200410060576 A CN200410060576 A CN 200410060576A CN 1323755 C CN1323755 C CN 1323755C
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- titanium dioxide
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- molecular sieve
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Abstract
Description
Numbering | Pore volume ml/g | Specific surface m 2/g | Crushing strength N/cm | Chemical composition, % | |||
CoO | WO 3 | MoO 3 | NiO | ||||
A B C D | 0.32 0.30 0.31 0.27 | 202 190 201 196 | 171 220 213 208 | / / / 3.9 | 15.0 15.0/ 1.8 | / 3.5 13.0 13.3 | 1.3 1.3 3.1 / |
Feedstock oil | Raw material I | Raw material II | Raw material II<80 ℃ | Raw material II>80 ℃ |
Boiling range, ℃ IBP/10% 50%/70% FBP sulphur, μ g/g group composition, % saturated hydrocarbons alkene aromatic hydrocarbons RON value | 38/64 103/135 194 1580 29.5 49.6 20.9 91.9 | 38/56 93/122 174 818 34.2 41.0 24.8 93.0 | 32/39 48/56 81 90 39.9 60.1 0 | 80/104 126/141 175 1090 26.3 32.6 42.1 |
The catalyst numbering | A | B | C | D |
Process conditions hydrogen dividing potential drop, the MPa temperature, ℃ liquid hourly space velocity (LHSV), h -1Hydrogen-oil ratio, v/v generates oil nature sulphur, μ g/g group composition, v% saturated hydrocarbons alkene aromatic hydrocarbons RON value liquid is received, % | 2.0 380 1.0 200 120 49.1 22.7 28.2 92.0 95.5 | 2.0 380 1.0 200 110 48.6 22.5 28.9 92.2 96.0 | 3.0 385 1.2 150 130 48.1 22.2 29.6 92.5 95.3 | 3.0 385 1.2 150 140 47.6 22.7 30.1 92.9 95.0 |
The catalyst numbering | A | B | C | D |
Process conditions hydrogen dividing potential drop, the MPa temperature, ℃ liquid hourly space velocity (LHSV), h -1Hydrogen-oil ratio, v/v ready-mixed oil character sulphur, μ g/g group composition, v% saturated hydrocarbons alkene aromatic hydrocarbons RON value liquid is received, % | 2.0 360 1.2 200 40 49.2 19.4 31.4 93.5 98.1 | 2.0 360 1.2 200 45 49.4 19.6 31.0 93.2 97.9 | 3.0 370 1.5 150 51 49.0 19.2 31.8 93.7 97.6 | 3.0 370 1.5 150 47 48.6 19.4 32.0 93.9 97.2 |
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2004100605763A CN1323755C (en) | 2004-10-18 | 2004-10-18 | Method for preparing hydrogenation aromatization catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2004100605763A CN1323755C (en) | 2004-10-18 | 2004-10-18 | Method for preparing hydrogenation aromatization catalyst |
Publications (2)
Publication Number | Publication Date |
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CN1621496A CN1621496A (en) | 2005-06-01 |
CN1323755C true CN1323755C (en) | 2007-07-04 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CNB2004100605763A Expired - Fee Related CN1323755C (en) | 2004-10-18 | 2004-10-18 | Method for preparing hydrogenation aromatization catalyst |
Country Status (1)
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CN (1) | CN1323755C (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104174429B (en) * | 2013-05-22 | 2017-08-25 | 中国石油化工股份有限公司 | A kind of method of heavy aromatic hydrocarbon light |
CN116515526B (en) * | 2022-01-20 | 2024-06-28 | 中国石油化工股份有限公司 | Hydrogenation-active metal desulfurization combined process for catalytically cracked gasoline |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5399258A (en) * | 1991-08-15 | 1995-03-21 | Mobil Oil Corporation | Hydrocarbon upgrading process |
US5413697A (en) * | 1991-08-15 | 1995-05-09 | Mobil Oil Corporation | Gasoline upgrading process |
US6042719A (en) * | 1998-11-16 | 2000-03-28 | Mobil Oil Corporation | Deep desulfurization of FCC gasoline at low temperatures to maximize octane-barrel value |
CN1356378A (en) * | 2001-09-26 | 2002-07-03 | 中国石油化工集团公司 | Hydrocatalyst and its preparing process |
CN1464033A (en) * | 2002-06-13 | 2003-12-31 | 中国科学院大连化学物理研究所 | Process for aromatization hydrogenation isomerization sulfur reduction modification of catalytically cracked gasoline |
CN1463792A (en) * | 2002-06-03 | 2003-12-31 | 北京石油化工学院材料与化工学院 | Novel molybdenum phosphorized hydrogenation desulfurization denitrification de-olefin catalyst and method for making same |
CN1488724A (en) * | 2002-10-10 | 2004-04-14 | 中国石油化工股份有限公司 | Aromatization modifying catalyst for catalytic gasoline and preocess |
-
2004
- 2004-10-18 CN CNB2004100605763A patent/CN1323755C/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5399258A (en) * | 1991-08-15 | 1995-03-21 | Mobil Oil Corporation | Hydrocarbon upgrading process |
US5413697A (en) * | 1991-08-15 | 1995-05-09 | Mobil Oil Corporation | Gasoline upgrading process |
US6042719A (en) * | 1998-11-16 | 2000-03-28 | Mobil Oil Corporation | Deep desulfurization of FCC gasoline at low temperatures to maximize octane-barrel value |
CN1356378A (en) * | 2001-09-26 | 2002-07-03 | 中国石油化工集团公司 | Hydrocatalyst and its preparing process |
CN1463792A (en) * | 2002-06-03 | 2003-12-31 | 北京石油化工学院材料与化工学院 | Novel molybdenum phosphorized hydrogenation desulfurization denitrification de-olefin catalyst and method for making same |
CN1464033A (en) * | 2002-06-13 | 2003-12-31 | 中国科学院大连化学物理研究所 | Process for aromatization hydrogenation isomerization sulfur reduction modification of catalytically cracked gasoline |
CN1488724A (en) * | 2002-10-10 | 2004-04-14 | 中国石油化工股份有限公司 | Aromatization modifying catalyst for catalytic gasoline and preocess |
Also Published As
Publication number | Publication date |
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CN1621496A (en) | 2005-06-01 |
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Address after: 100029 Beijing City, Chaoyang District Hui Street No. 6 Co-patentee after: Luoyang Petrochemical Engineering Corporation /SINOPEC Patentee after: China Petrochemical Group Corp. Address before: 100029 Beijing City, Chaoyang District Hui Street No. 6 Co-patentee before: Luoyang Petrochemical Engineering Co., China Petrochemical Group Patentee before: China Petrochemical Group Corp. |
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Free format text: FORMER OWNER: SINOPEC LUOYANG PETROCHEMICAL ENGINEERING CORPORATION Effective date: 20130326 Owner name: SINOPEC LUOYANG PETROCHEMICAL ENGINEERING CORPORAT Free format text: FORMER OWNER: SINOPEC GROUP Effective date: 20130326 |
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Effective date of registration: 20130326 Address after: 471003 Zhongzhou West Road, Henan, China, No. 27, No. Patentee after: Luoyang Petrochemical Engineering Corporation /SINOPEC Address before: 100029 Beijing City, Chaoyang District Hui Street No. 6 Patentee before: China Petrochemical Group Corp. Patentee before: Luoyang Petrochemical Engineering Corporation /SINOPEC |
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